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H Grijseels

Publications and source records attributed to H Grijseels.

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Dissolution of theophylline monohydrate and anhydrous theophylline in buffer solutions.

The dissolution kinetics of theophylline monohydrate and anhydrous theophylline were investigated with a rotating-disk apparatus in buffer solutions at 298 K under sink conditions. The observed dissolution rate of theophylline monohydrate under various conditions agreed well with predictions based on the Extended Simultaneous Chemical Reaction and Dissolution concept. Below 337 K, anhydrous theophylline is converted to theophylline monohydrate in contact with water. The dissolution profile of anhydrous theophylline can be divided into three phases: a pre-transformation phase: anhydrous theophylline dissolves; the transformation phase, during which its dissolution rate drops to the level of the theophylline monohydrate dissolution rate; and steady state, at which the dissolution rate of anhydrous theophylline equals the dissolution rate of theophylline monohydrate. The presence of theophylline monohydrate crystals at the dissolving surface was confirmed by IR spectroscopy and microscopic observation. The length of the transformation phase, depending on the characteristics of the diffusion boundary layer, varied with the experimental conditions (e.g., pH and rotation speed). It was concluded that during the dissolution process the disk is covered with theophylline monohydrate crystals that precipitate from the supersaturated medium adjacent to the disk surface, and that crystallization of theophylline monohydrate is a precipitation process controlled by hydrodynamic and diffusion parameters.

Buffers

Dissolution at porous interfaces VI: Multiple pore systems.

With the aid of rapidly dissolving sodium chloride particles, cubic pores were made in the surface of a theophylline tablet. The influence of the pores on the dissolution rate of the surface was investigated in a rotating disk apparatus. Like the drilled pores used in earlier studies, downstream on the surface they caused a turbulent flow regimen with the development of a trough due to enhanced erosion. The phenomenon of a critical pore diameter, discovered with single, drilled pores, seems to be applicable to the cubic pores investigated in this study, although a higher degree of surface coverage with pores caused complications, probably due to particles bordering one another and forming larger pores. The behavior of the porous surfaces at different rotation speeds was studied. Due to the presence of pores the laminar character of the boundary layer flow changes to turbulent, which induces locally an increased dissolution flux in the wake of a pore.

Particle Size

Dissolution at porous interfaces. IV. Pore effects in natural convection flow.

The dissolution rate of a nicotinic acid tablet surface was measured in a dissolution system where mass transport in the solvent is governed by a combination of natural and forced convection. While such experimental conditions were chosen that natural convection outweighted forced convection, the dissolution rate increasing effect of large pores in the tablet surface was studied. To that end cylindrical pores were drilled into the tablet. The increase in dissolution rate was measured as a function of the number of pores, their depth and diameter and their position with respect to each other and to the centre of the dissolving surface. The results are discussed with regard to the hydrodynamic conditions near the pores. In addition to the regularly arranged cylindrical pores a more irregular configuration of cubic pores was investigated. These pores were created by embedding cubic sodium chloride crystals in the tablet surface during the compression procedure. After the sodium chloride particles had dissolved rapidly a porous surface of much slower dissolving nicotinic acid remained. The dissolution rate of the porous surface was determined and a comparison was made between surfaces with and without pores of several sizes.

Nicotinic Acids